GB633334A - Improvements in or relating to the partial oxidation of hydrocarbons in the vapour phase - Google Patents
Improvements in or relating to the partial oxidation of hydrocarbons in the vapour phaseInfo
- Publication number
- GB633334A GB633334A GB2598/43A GB259843A GB633334A GB 633334 A GB633334 A GB 633334A GB 2598/43 A GB2598/43 A GB 2598/43A GB 259843 A GB259843 A GB 259843A GB 633334 A GB633334 A GB 633334A
- Authority
- GB
- United Kingdom
- Prior art keywords
- reactor
- suspended
- contact material
- oxidation
- returned
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/22—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds
- C01B3/24—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons
- C01B3/28—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons using moving solid particles
- C01B3/30—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons using moving solid particles using the fluidised bed technique
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
- C01B3/42—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts using moving solid particles
- C01B3/44—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts using moving solid particles using the fluidised bed technique
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
<PICT:0633334/III/1> The partial oxidation of hydrocarbons in the vapour phase is effected by passing the vapour upwardly through a reaction zone A p containing a dense pseudo-liquid phase of finely-divided contact material, the velocity being such that a substantial proportion of the latter is carried out of the reactor in suspension in the reaction products, whereby their temperature is maintained uniform. The entrained particles are separated from the reaction products by cyclons 13, 14 and returned to the reactor. Contact material may also be withdrawn from the dense phase by conduits 11 and either suspended in a part of the reaction gas and returned to the reactor after passage through a heater or cooler 26, or suspended, e.g. in air and passed through a regenerator A1 resembling the reactor in construction, the regenerated material being suspended in feed gas in pipe 4 and recycled. The contact material may be a catalyst, e.g. vanadium pentoxide, an oxidising agent such as copper oxide, or an inert material maintaining temperature control. Reactions described are the catalytic oxidation of naphthalene to phthalic anhydride and the oxidation of methane to formaldehyde by means of copper oxide. The conversion of aliphatic and aromatic hydrocarbons in general to alcohols, aldehydes, ketones, acids, &c. is mentioned. The Specification as open to inspection under Sect. 91 comprises also the extension of the invention to vapour phase reactions in general but includes no further specific examples. This subject-matter does not appear in the Specification as accepted.ALSO:The partial oxidation of hydrocarbons in the vapour phase is effected by passing the vapour upwardly through a reaction zone A containing a dense pseudo-liquid phase of finely-divided contact material, the velocity being such that a substantial proportion of the latter is carried out of the reactor in suspension in the reaction products, whereby their temperature is maintained uniform. The entrained particles are separated from the reaction products by cyclones 13, 14 and returned to the reactor. Contact material may also be withdrawn from the dense phase by conduits 11 and <PICT:0633334/IV (b)/1> either suspended in a part of the reaction gas and returned to the reactor after passage through a heater or cooler 26, or suspended, e.g. in air, and passed through a regenerator A1 resembling the reactor in construction, the regenerated material being suspended in feed gas in pipe 4 and recycled. The contact material may be a catalyst, an oxidizing agent such as copper oxide, or an inert material maintaining temperature control. Reactions described are the catalytic oxidation of naphthalene to phthalic anhydride and the oxidation of methane to formaldehyde by means of copper oxide. The conversion of aliphatic and aromatic hydrocarbons in general to unsaturated hydro carbons, alcohols, aldehydes, ketones, and acids, is referred to with specific mention of acetylene, butene, butadiene, maleic acid, and benzoic acid as products.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US633334XA | 1942-04-23 | 1942-04-23 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB633334A true GB633334A (en) | 1949-12-12 |
Family
ID=22048490
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2598/43A Expired GB633334A (en) | 1942-04-23 | 1943-02-16 | Improvements in or relating to the partial oxidation of hydrocarbons in the vapour phase |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB633334A (en) |
-
1943
- 1943-02-16 GB GB2598/43A patent/GB633334A/en not_active Expired
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